(19) |
 |
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(11) |
EP 0 055 920 A3 |
(12) |
EUROPEAN PATENT APPLICATION |
(88) |
Date of publication A3: |
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22.09.1982 Bulletin 1982/38 |
(43) |
Date of publication A2: |
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14.07.1982 Bulletin 1982/28 |
(22) |
Date of filing: 23.12.1981 |
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(84) |
Designated Contracting States: |
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BE CH DE FR GB IT LI LU NL SE |
(30) |
Priority: |
02.01.1981 US 222196
|
(71) |
Applicant: The Standard Oil Company |
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() |
|
(72) |
Inventors: |
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- Presson, Robert Dean
()
- Wu, Hsin-Chih
()
- Sockell, Edward J.
()
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(54) |
Process for the continuous recovery of acetonitrile |
(57) A continuous process for recovering highly pure acetonitrile from crude acetonitrile
containing acetonitrile, water, HCN and heavy organics, said process comprising:
(1) distilling said crude acetonitrile in a first distillation zone at a first pressure
at or above 1 atmosphere to remove HCN therefrom and produce a first acetonitrile/water
azeotrope and a first bottoms product containing water,
(2) distilling said first azeotrope in a second distillation zone at a second pressure
less than 1 atmosphere to separate said first azeotrope into a second bottoms product
containing water and a second acetonitrile/water azeotrope having a greater acetonitrile
concentration than said first azeotrope, and
(3) distilling said second acetonitrile/water azeotrope in a third distillation zone
at a third pressure above 1 atmosphere to produce a third acetonitrile/water azeotrope
containing substantially all of the water in said second azeotrope, third bottoms
product comprising acetonitrile and heavy organics and a sidestream comprising said
highly pure acetonitrile.
This process enables one to obtain acetonitrile in 99+% purity. It is based upon a
continuous distillation process carried out in three stages at three different pressures.
